US4039619A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for the selective removal of hydrogen sulfide from hot coal gasification gases
Assignee: Foster Wheeler Energy Corp
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Filing: 1975-11-04
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Granted: 1977-08-02
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Expires: 1995-11-04
Abstract
Abstract Continuous process for the selective removal of hydrogen sulfide from a mixture of hot coal gasification gases containing hydrogen sulfide by contacting such mixture in a reaction or desulfurizing zone at an elevated temperature with a nickel-containing material whereby the nickel reacts with the hydrogen sulfide to form solid compounds from which the nickel content can be regenerated by oxidation and recycled back to the reaction zone, thereby effectively removing hydrogen sulfide from the hot gas mixture.
Inventors
- 👤 Peter Steiner
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 10:36
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/52
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
114 words
A process for the selective removal of hydrogen sulfide from hot coal gasification effluent gases containing same, comprising contacting a hydrogen sulfide-containing coal gasification effluent gas in a reaction zone containing a solid nickel acceptor at a temperature range between about 1000° F. and about 1450° F. whereby said nickel acceptor is at least partially sulfided; withdrawing the sulfided nickel acceptor from the reaction zone to a regenerating zone; and subjecting the sulfided nickel acceptor to a source of oxygen at a temperature which is approximately the same as that in the reaction zone, said temperature being from about 1000° F. to about 1450° F., thereby forming sulfur dioxide and a regenerated nickel acceptor.
Claim 2
Dependent Claim
114 words
A process for the selective removal of hydrogen sulfide from hot coal gasification effluent gases containing same, comprising contacting a hydrogen sulfide-containing coal gasification effluent gas in a reaction zone containing a solid nickel acceptor at a temperature range between about 1000° F. and about 1450° F. whereby said nickel acceptor is at least partially sulfided; withdrawing the sulfided nickel acceptor from the reaction zone to a regenerating zone; and subjecting the sulfided nickel acceptor to a source of oxygen at a temperature which is approximately the same as that in the reaction zone, said temperature being from about 1000° F. to about 1450° F., thereby forming sulfur dioxide and a regenerated nickel acceptor.
Claim 3
Dependent Claim
23 words
A process according to claim 1 wherein the temperature range in said reaction zone is between about 1000° F. and about 1350° F.
Claim 4
Dependent Claim
19 words
A process according to claim 2 wherein the temperature range is between about 1000° F. and about 1150° F.
Claim 5
Dependent Claim
23 words
A process according to claim 1 wherein the temperature range in said regenerating zone is between about 1050° F. and about 1350° F.
Claim 6
Dependent Claim
19 words
A process according to claim 4 wherein the temperature range is between about 1050° F. and about 1150° F.
Claim 7
Dependent Claim
40 words
A process according to claim 1 wherein the temperature range in said reaction zone is between about 1000° F. and about 1350° F. and the temperature range in said regenerating zone is between about 1050° F. and about 1350° F.
Claim 8
Dependent Claim
128 words
A continuous process for the selective removal of hydrogen sulfide from hot coal gasification effluent gases containing same, comprising contacting a hydrogen sulfide-containing coal gasification effluent gas in a reaction zone containing a solid nickel acceptor at a temperature range between about 1000° F. and about 1450° F. whereby said acceptor is at least partially sulfided; withdrawing the sulfided acceptor from the reaction zone to a regenerating zone; subjecting the sulfided acceptor to a source of oxygen at a temperature which is approximately the same as that in the reaction zone, said temperature being from about 1000° F. and about 1450° F., thereby forming sulfur dioxide and a regenerated nickel acceptor; removing sulfur dioxide from the regeneration zone; and supplying the regenerated nickel acceptor to the reaction zone.
Claim 9
Dependent Claim
128 words
A continuous process for the selective removal of hydrogen sulfide from hot coal gasification effluent gases containing same, comprising contacting a hydrogen sulfide-containing coal gasification effluent gas in a reaction zone containing a solid nickel acceptor at a temperature range between about 1000° F. and about 1450° F. whereby said acceptor is at least partially sulfided; withdrawing the sulfided acceptor from the reaction zone to a regenerating zone; subjecting the sulfided acceptor to a source of oxygen at a temperature which is approximately the same as that in the reaction zone, said temperature being from about 1000° F. and about 1450° F., thereby forming sulfur dioxide and a regenerated nickel acceptor; removing sulfur dioxide from the regeneration zone; and supplying the regenerated nickel acceptor to the reaction zone.
Claim 10
Dependent Claim
47 words
A continuous process according to claim 2 wherein the regenerated nickel acceptor is continuously supplied to the reaction zone to maintain the nickel and nickel sulfide composition therein constant for a constant rate of sulfur removal from the hot coal gasification effluent gas in said reaction zone.
Claim 11
Dependent Claim
36 words
A continuous process according to claim 2 wherein the hot coal gasification effluent gas is fed into the reaction zone at a temperature close to the desulfurization temperature, thereby keeping said reaction zone in heat balance.
Claim 12
Dependent Claim
40 words
A continuous process according to claim 2 wherein the regeneration of the nickel acceptor is effected at a temperature sufficient to satisfy the equilibrium considerations governing the regeneration reaction as well as the reaction between Ni and SO 2 .
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-08-01 | 1981-01-31 | 1981-08-02 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-08-01 | 1985-01-31 | 1985-08-02 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-08-01 | 1989-01-31 | 1989-08-02 | $7700.00 | Window Closed / Lapsed |